首页> 外文会议>ASME Pressure Vessels and Piping Division/K-PVP conference;PVP2010 >NUMERICAL ANALSIS ON CONVECTION HEAT TRANSFER OF PULSTING FLOW IN A CORRUGATED TUBE
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NUMERICAL ANALSIS ON CONVECTION HEAT TRANSFER OF PULSTING FLOW IN A CORRUGATED TUBE

机译:波纹管内脉动流对流换热的数值分析

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Heat transfer enhancement of corrugated tube in Laminar flow was studied using CFD. Numerical calculation performed with grids of increasing density confirms that the grids are independent. In order to get the optimal numerical calculation the boundary layer was refined. The final grid consisted of 146,000 computational cells. The fluid inlet was defined as a velocity inlet with a sinuaoidal pulasating flow input. The outlet was modeled as a pressure-outlet.By numerical simulation, the distribution of velocity and temperature of the corrugated tube of different conditions in different Reynolds number(380~1900) of steady flow ,and the vibration frequency (50-200HZ)and the vibration amplitude of sinusoidal (0.1—0.9) pulsating flow is analysed, thus the characteristics of distribution of velocity and temperature are demonstrated. Thesimulation result indicates that by comparing with the steady flow, the pulsating flow increases the heat transfer efficiency of the corrugated tube in Laminar flow by 83% for most. The enhancement is due to the pulsating flow increating vortex. The vortex result in increasrs disturbance, decreasing the thermal boundary layer thickness, enhancing heat transfer of the corrugated tube. The result also shows that enhancement of heat transfer coefficient inceases as the velocity rises in a certain range ,and it also increases as the frequency rises before reaching the peak point and then decreases as the vibration frequency rises in a certain range. Under the condition of none-backflow, the velocity of increasing enhancement of heat transfer coefficient becomes slower and slower as the vibration amplitude rises. In our study, the best dimensionless pulsating frequencies of thecorrugated tube are 100-200 HZ and the amplitudes are 0.4~0.6 , when condition that the Reynolds number is ranged from 380 to 1900.
机译:利用CFD研究了层流中波纹管的传热增强。用密度增加的网格进行的数值计算证实了网格是独立的。为了获得最佳数值计算,对边界层进行了细化。最终的网格由146,000个计算单元组成。流体入口定义为具有正弦脉动流输入的速度入口。通过数值模拟,研究了在不同雷诺数(380〜1900)稳定流,振动频率(50-200HZ)和不同振动频率下,不同条件下波纹管的速度和温度的分布情况。分析了正弦波(0.1—0.9)脉动流的振幅,从而证明了速度和温度分布的特征。这 仿真结果表明,与稳定流相比,脉动流在层流中最大程度地提高了波纹管的传热效率,达83%。增强是由于产生涡流的脉动流。涡流导致扰动增加,减小了热边界层的厚度,增强了波纹管的热传递。结果还表明,随着速度在一定范围内的增大,传热系数的增大也随之增大;在到达峰值点之前,随着频率的增大,传热系数的增大也随之增大;随着振动频率在一定范围内的增大,传热系数的增大也减小。在无回流的条件下,随着振动幅度的增加,传热系数的增大增强速度越来越慢。在我们的研究中,当雷诺数在380至1900范围内时,波纹管的最佳无量纲脉动频率为100-200 HZ,幅度为0.4〜0.6。

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